CN108469803A - It safeguards judge index apparatus for predicting, volume control device and safeguards judge index estimating method - Google Patents
It safeguards judge index apparatus for predicting, volume control device and safeguards judge index estimating method Download PDFInfo
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Abstract
Description
技术领域technical field
本发明涉及一种对质量流量控制器等流量控制装置和过滤器等相关设备是否需要维护的判断指标进行推断的技术。The invention relates to a technology for inferring the judgment index of whether flow control devices such as mass flow controllers and related equipment such as filters need to be maintained.
背景技术Background technique
在半导体制造装置等中,为了将材料气体等以一定流量导入至真空腔室内,采用有图6所示那样的质量流量控制器等流量控制装置(参考专利文献1)。在图6中,100为主体块,101为传感器组件,102为传感器组件101的头部,103为搭载于头部102的流体传感器,104为阀,105为形成于主体块100的内部的流路,106为流路105的入口侧的开口,107为流路105的出口侧的开口。In semiconductor manufacturing equipment and the like, a flow control device such as a mass flow controller as shown in FIG. 6 is used to introduce a material gas or the like into a vacuum chamber at a constant flow rate (refer to Patent Document 1). In FIG. 6 , 100 is a main body block, 101 is a sensor unit, 102 is a head of the sensor unit 101, 103 is a fluid sensor mounted on the head 102, 104 is a valve, and 105 is a fluid flow sensor formed inside the main body block 100. 106 is an opening on the inlet side of the flow path 105 , and 107 is an opening on the outlet side of the flow path 105 .
流体从开口106流入至流路105并通过阀104而从开口107排出。流体传感器103测量在流路105中流动的流体的流量。质量流量控制器的未图示的控制电路以流体传感器103所测量出的流体的流量与设定值一致的方式驱动阀104。The fluid flows into the flow path 105 from the opening 106 and is discharged from the opening 107 through the valve 104 . The fluid sensor 103 measures the flow rate of fluid flowing in the flow path 105 . A not-shown control circuit of the mass flow controller drives the valve 104 so that the flow rate of the fluid measured by the fluid sensor 103 coincides with a set value.
当通过这种质量流量控制器来持续进行材料气体的流量控制时,材料气体中所含的成分的影响等有时会导致污物附着于质量流量控制器本身或者材料气体的流路上配备的过滤器等相关设备等而发生故障。When the flow rate of the material gas is continuously controlled by such a mass flow controller, the influence of the components contained in the material gas may cause contamination to adhere to the mass flow controller itself or to the filter provided on the flow path of the material gas. and other related equipment and so on.
因此,提出一种以在质量流量控制器中内置的流体传感器的整个测定范围内只在容许精度范围内产生流量误差、压力误差的方式来操作、校正阀开度的装置(参考专利文献2)。然而,在专利文献2所揭示的诊断机构中,存在如下问题:虽然能够诊断流体传感器的测量值与实际的流量的误差是否是在精度上能够容许的程度,但为了诊断,需要将设置于流路上的阀维持为全闭状态,或者使阀从全闭状态变化为开发状态,在装置的运行中难以进行诊断。在质量流量控制器例如被设置在半导体制造装置的情况下,难以为了进行质量流量控制器的诊断而使半导体制造装置整体停止。Therefore, a device for correcting the valve opening by operating and correcting the valve opening has been proposed so that flow rate errors and pressure errors occur only within the allowable accuracy range over the entire measurement range of the fluid sensor built in the mass flow controller. . However, in the diagnostic mechanism disclosed in Patent Document 2, there is a problem that although it is possible to diagnose whether the error between the measured value of the fluid sensor and the actual flow rate is tolerable in accuracy, it is necessary to install The valve on the road is kept in a fully closed state, or the valve is changed from a fully closed state to a developed state, making it difficult to diagnose during the operation of the device. When the mass flow controller is installed in, for example, a semiconductor manufacturing apparatus, it is difficult to stop the entire semiconductor manufacturing apparatus for diagnosis of the mass flow controller.
此外,在专利文献2所揭示的诊断机构中,存在如下的问题:当在半导体制造装置的运行停止的时刻进行质量流量控制器的诊断的情况下,在该运行停止期间,在使流体流入质量流量控制器的流路之后需要使阀变化为全闭状态,诊断作业花费工夫。在半导体制造装置等中,如果能够在装置的运行中判断维护的必要性,则进行运行管理会变得容易,因此寻求改进。In addition, in the diagnosis mechanism disclosed in Patent Document 2, when the diagnosis of the mass flow controller is performed at the time when the operation of the semiconductor manufacturing apparatus is stopped, there is a problem in that the flow of the fluid into the mass flow controller occurs during the stop of the operation. Afterwards, the flow path of the flow controller needs to change the valve to the fully closed state, and the diagnostic work takes time and effort. In semiconductor manufacturing equipment and the like, if the necessity of maintenance can be judged during the operation of the equipment, it will be easier to perform operation management, so improvement is sought.
现有技术文献prior art literature
专利文献patent documents
专利文献1:日本专利特开2008-039588号公报Patent Document 1: Japanese Patent Laid-Open No. 2008-039588
专利文献2:日本专利第5931668号公报Patent Document 2: Japanese Patent No. 5931668
发明内容Contents of the invention
发明要解决的问题The problem to be solved by the invention
本发明为了解决上述问题而做出,其目的在于提供一种能够在装置的运行中对流量控制装置及其相关设备是否需要维护的判断指标进行推断的维护指标推断装置、流量控制装置及维护指标推断方法。The present invention is made to solve the above problems, and its purpose is to provide a maintenance index estimation device, a flow control device and a maintenance index that can infer whether the flow control device and its related equipment need to be maintained during the operation of the device. Inference method.
解决问题的技术手段technical means to solve problems
本发明的维护判断指标推断装置的特征在于,具备:阀开度获取部,其构成为获取在使用阀来控制流体的流量的流量控制中所述流体的流量被维持在预先规定的目标流量时的所述阀的开度;以及流量上限推断部,其构成为基于对所述阀的开度与所述流体的流量的关系加以近似而得的函数以及由所述阀开度获取部获取到的所述阀的开度,将假定在该获取的时间点所述阀的开度达到上限的情况下的流量上限值推断为流量控制装置的维护判断指标。The maintenance judgment index estimating device of the present invention is characterized by comprising: a valve opening acquisition unit configured to acquire when the flow rate of the fluid is maintained at a predetermined target flow rate in the flow rate control using a valve to control the flow rate of the fluid; the opening degree of the valve; and a flow upper limit estimation unit configured based on a function obtained by approximating the relationship between the opening degree of the valve and the flow rate of the fluid and obtained by the valve opening degree acquisition unit The opening degree of the valve is estimated as the maintenance judgment index of the flow control device by assuming that the opening degree of the valve reaches the upper limit at the acquired time point.
此外,本发明的维护判断指标推断装置的1构成例的特征在于,所述流量上限推断部将与所述流量上限值对应的所述阀的开度的上限设为100%。In addition, a configuration example of the maintenance judgment index estimation device of the present invention is characterized in that the flow rate upper limit estimation unit sets the upper limit of the opening degree of the valve corresponding to the flow rate upper limit value to 100%.
此外,本发明的维护判断指标推断装置的1构成例的特征在于,所述函数至少由与所述阀的开度有关的项和作为与该项相乘的数值的增益来加以定义,所述流量上限推断部基于假定所述增益随着时间的经过而减少时从所述函数获得的数式以及由所述阀开度获取部获取到的所述阀的开度,来推断所述流量上限值。In addition, a configuration example of the maintenance judgment index estimating device of the present invention is characterized in that the function is defined by at least a term related to the opening degree of the valve and a gain which is a numerical value multiplied by the term, and the The flow rate upper limit estimation unit estimates the flow rate upper limit based on an expression obtained from the function assuming that the gain decreases with time and the opening degree of the valve acquired by the valve opening degree acquisition unit. value.
此外,本发明的维护判断指标推断装置的1构成例的特征在于,所述函数是对所述阀的开度与所述流体的流量的非线性关系加以近似而得的函数,与所述阀的开度有关的项使用指数函数表示。In addition, a configuration example of the maintenance judgment index estimation device of the present invention is characterized in that the function is a function obtained by approximating a nonlinear relationship between the opening degree of the valve and the flow rate of the fluid, and is similar to that of the valve. The opening-related terms are expressed using exponential functions.
此外,本发明的维护判断指标推断装置的1构成例的特征在于,所述函数是对所述阀的开度与所述流体的流量的非线性关系加以近似而得的函数,与所述阀的开度有关的项使用分数函数表示。In addition, a configuration example of the maintenance judgment index estimation device of the present invention is characterized in that the function is a function obtained by approximating a nonlinear relationship between the opening degree of the valve and the flow rate of the fluid, and is similar to that of the valve. The opening-related terms are expressed using fractional functions.
此外,本发明的维护判断指标推断装置的1构成例的特征在于,所述流量上限推断部由增益算出部和流量上限算出部构成,该增益算出部基于在想要推断所述流量上限值的当前时间点由所述阀开度获取部获取到的所述阀的开度和所述目标流量,算出当前时间点的所述增益,该流量上限算出部基于由该增益算出部算出的增益来算出所述流量上限值。In addition, one configuration example of the maintenance judgment index estimation device of the present invention is characterized in that the flow rate upper limit estimation unit is composed of a gain calculation unit and a flow rate upper limit calculation unit, and the gain calculation unit estimates the flow rate upper limit value based on At the current time point, the valve opening obtained by the valve opening acquisition unit and the target flow rate are used to calculate the gain at the current time point, and the flow rate upper limit calculation unit is based on the gain calculated by the gain calculation unit To calculate the flow upper limit.
此外,本发明的维护判断指标推断装置的1构成例的特征在于,还具备对由所述流量上限推断部推断出的流量上限值进行数值显示的推断结果输出部。In addition, one configuration example of the maintenance judgment index estimating device according to the present invention further includes an estimation result output unit for numerically displaying the upper limit value of the flow rate estimated by the upper limit estimating unit.
此外,本发明的维护判断指标推断装置的1构成例的特征在于,还具备在由所述流量上限推断部推断出的流量上限值不满预先规定的阈值时发出警报的推断结果输出部。In addition, one configuration example of the maintenance judgment index estimating device of the present invention further includes an estimation result output unit that issues an alarm when the flow rate upper limit value estimated by the flow rate limit estimating unit is less than a predetermined threshold value.
此外,本发明的流量控制装置的特征在于,具备:流量测量部,其测量在流路中流动的流体的流量;阀,其被设置在所述流路上;流量控制部,其操作所述阀,以使由所述流量测量部测量出的所述流量与预先规定的目标流量一致;以及维护判断指标推断装置,并且,所述维护判断指标推断装置的所述阀开度获取部获取在所述流路上设置的所述阀的开度。In addition, the flow control device of the present invention is characterized in that it includes: a flow measurement unit that measures the flow rate of fluid flowing in the flow path; a valve that is provided on the flow path; and a flow control unit that operates the valve. so that the flow rate measured by the flow rate measurement unit coincides with a predetermined target flow rate; and maintenance judgment index estimation means, and the valve opening degree acquisition unit of the maintenance judgment index estimation means acquires the The opening degree of the valve provided on the flow path.
此外,本发明的维护判断指标推断方法的特征在于,包含:第1步骤,获取在使用阀来控制流体的流量的流量控制中所述流体的流量被维持在预先规定的目标流量时的所述阀的开度;以及第2步骤,基于对所述阀的开度与所述流体的流量的关系加以近似而得的函数以及由所述第1步骤获取到的所述阀的开度,将假定在该获取的时间点所述阀的开度达到上限的情况下的流量上限值推断为流量控制装置的维护判断指标。In addition, the maintenance judgment index estimation method of the present invention is characterized by including: a first step of acquiring the flow rate of the fluid when the flow rate of the fluid is maintained at a predetermined target flow rate in the flow control using a valve to control the flow rate of the fluid; the opening degree of the valve; and the second step, based on the function obtained by approximating the relationship between the opening degree of the valve and the flow rate of the fluid and the opening degree of the valve obtained by the first step, The upper limit value of the flow rate when the opening degree of the valve reaches the upper limit at the acquired time point is estimated as a maintenance judgment index of the flow rate control device.
发明的效果The effect of the invention
根据本发明,能够在装置的运行中推断流量控制及其相关设备是否需要维护的判断指标(流量上限值)。其结果是,对于操作人员而言,容易进行设置有流量控制装置的半导体制造装置等的运行管理。此外,在本发明中,能够大幅降低是否需要维护的判断所花费的工夫。According to the present invention, it is possible to infer the judgment index (flow upper limit value) of whether the flow control and its related equipment need to be maintained during the operation of the device. As a result, it is easy for the operator to perform operation management of the semiconductor manufacturing equipment and the like provided with the flow rate control device. In addition, in the present invention, it is possible to significantly reduce the time and effort required to determine whether or not maintenance is necessary.
附图说明Description of drawings
图1是表示在质量流量控制器中设置的阀的开度与流体的流量的关系的一例的图。FIG. 1 is a diagram showing an example of the relationship between the opening degree of a valve provided in a mass flow controller and the flow rate of a fluid.
图2是表示在质量流量控制器中设置的阀的开度与流体的流量的关系的另一例的图。2 is a diagram showing another example of the relationship between the opening degree of a valve provided in the mass flow controller and the flow rate of a fluid.
图3是表示本发明的实施例所涉及的流量控制装置的构成的框图。FIG. 3 is a block diagram showing the configuration of a flow control device according to an embodiment of the present invention.
图4是说明本发明的实施例所涉及的流量控制装置的流量控制动作的流程图。FIG. 4 is a flowchart illustrating the flow control operation of the flow control device according to the embodiment of the present invention.
图5是说明本发明的实施例所涉及的流量控制装置的维护判断指标推断动作的流程图。FIG. 5 is a flowchart illustrating the maintenance judgment index estimation operation of the flow rate control device according to the embodiment of the present invention.
图6是质量流量控制器的截面图。Fig. 6 is a cross-sectional view of a mass flow controller.
具体实施方式Detailed ways
大多数情况下,质量流量控制器的用途是将流体的流量稳定地维持在预先以限定方式决定的目标流量。因而,若以这种用途为前提,则能以可靠性较高的检测条件推断过滤器的堵塞的影响等。具体而言,检测被稳定地维持在任意的目标流量的状态,并获取该条件下的阀开度指示信号。In most cases, the purpose of a mass flow controller is to maintain a steady flow of fluid at a target flow rate determined in a predetermined manner. Therefore, on the premise of such a use, it is possible to estimate the influence of clogging of the filter, etc. under a highly reliable detection condition. Specifically, a state in which an arbitrary target flow rate is stably maintained is detected, and a valve opening indication signal under this condition is acquired.
若考虑发生了设置在质量流量控制器的上游的过滤器的堵塞的情况,则在该时间点使阀开度饱和到100%的状态下可达到的流量是该时间点的可控制的流量的上限值,换言之,推断该上限值并判断是否进行维护是有效的。因此,发明者想到,基于质量流量控制器特有的使用条件,获取可靠性较高的阀开度的信息,并将从中推断的流量上限值(例如阀开度100%时的推断流量)作为是否需要维护的判断指标是妥当的。Considering the clogging of the filter installed upstream of the mass flow controller, the flow rate that can be achieved in the state where the valve opening is saturated to 100% at this point in time is the controllable flow rate at that point in time. The upper limit value, in other words, it is effective to infer the upper limit value and judge whether to perform maintenance. Therefore, the inventor conceived the idea of acquiring highly reliable valve opening information based on the unique operating conditions of the mass flow controller, and using the flow rate upper limit value estimated therefrom (for example, the estimated flow rate when the valve opening is 100%) as The judgment indicator of whether maintenance is required is appropriate.
[实施例][Example]
下面,参考附图对于本发明的实施例进行说明。在专利文献2中示出了如下内容:在使设置于质量流量控制器中的阀的开度在时间上呈线性变化的情况下,越是高开度侧,在流路中流动的流体的流量体积的变化越少。由此可知,阀开度MV与流量PV为非线性关系,越是高开度侧,相对于开度MV的变化量而言,流量PV的变化量越是减少。这种质量流量控制器的特性的概略示于图1。再者,在图1的例子中,将流量PV归一化为0~100%的值。图1所示那样的特性为非线性收敛现象,因此能以下式的指数函数来表现。Embodiments of the present invention will be described below with reference to the drawings. Patent Document 2 shows that when the opening degree of a valve provided in a mass flow controller is changed linearly with time, the higher the opening degree side, the lower the flow rate of the fluid flowing in the flow path. The less the flow volume changes. It can be seen from this that the valve opening degree MV and the flow rate PV have a nonlinear relationship, and the higher the opening degree side, the smaller the change amount of the flow rate PV relative to the change amount of the opening degree MV. The outline of the characteristics of this mass flow controller is shown in FIG. 1 . In addition, in the example of FIG. 1, the flow rate PV is normalized to the value of 0-100%. The characteristic shown in FIG. 1 is a nonlinear convergence phenomenon, so it can be expressed by the exponential function of the following formula.
PV=K{1.0-exp(-MV/A)}···(1)PV=K{1.0-exp(-MV/A)}···(1)
如此,对阀开度MV与流量PV的关系加以近似而得的函数由常数项(1.0)、与阀开度MV有关的项、以及作为与这各项相乘的数值的增益K加以定义。式(1)的A为赋予非线性收敛状态的系数。图1的曲线cur1表示质量流量控制器的初始特性。以能够预先掌握的供给压力为基准,设定在阀开度MV=100%时流量PV达到最大值100%,此外,结合普通的非线性的图像,曲线cur1能以下式那样的系数值的指数函数来表现。Thus, a function approximating the relationship between the valve opening MV and the flow rate PV is defined by a constant term (1.0), a term related to the valve opening MV, and a gain K that is a numerical value multiplied by these terms. A in Equation (1) is a coefficient that gives a nonlinear convergence state. The curve cur1 of Fig. 1 represents the initial characteristic of the mass flow controller. Based on the supply pressure that can be grasped in advance, set the flow rate PV to reach the maximum value of 100% when the valve opening MV = 100%. In addition, combined with ordinary nonlinear images, the curve cur1 can be an index of the coefficient value like the following formula function to perform.
PV=104.0{1.0-exp(-MV/30.0)}···(2)PV=104.0{1.0-exp(-MV/30.0)}···(2)
式(2)的K=104.0、A=30.0为这些数值的1例。在设置于流路上的过滤器等的堵塞现象中,能够推断处于该过滤器的下游的质量流量控制器的阀本身的特性即非线性是不会变化的,因此,系数A可以视为固定。因此,假定只有增益K会因为过滤器的堵塞现象等而减少。K=104.0 and A=30.0 in the formula (2) are one example of these numerical values. In the case of clogging of a filter or the like installed on the flow path, it can be inferred that the characteristic of the mass flow controller downstream of the filter, that is, the nonlinearity of the valve itself does not change, so the coefficient A can be regarded as fixed. Therefore, it is assumed that only the gain K decreases due to clogging of the filter or the like.
在判断质量流量控制器、质量流量控制器的相关设备是否需要维护之后,虽然推测若干因素会对质量流量控制器的运行时间产生影响,但假定增益K以与运行时间大致成比例的形式、即以没有急剧恶化的程度的一定的缓和的速度减少较为妥当。After judging whether the mass flow controller and related equipment of the mass flow controller need to be maintained, although it is speculated that several factors will affect the running time of the mass flow controller, it is assumed that the gain K is roughly proportional to the running time, that is, It is more appropriate to reduce at a certain moderate rate without a sharp deterioration.
此处,将预先规定的目标流量PVx假定为PVx=60.0%。即,作为质量流量控制器的流量设定值SP而赋予的最基准的数值为SPx=60.0%。若将用于使流体的流量整定为PVx=60.0%的质量流量控制器的初始状态的阀开度设为MV1,则根据曲线cur1,MV1=25.8%。由于可以预先掌握非线性特性的系数A=30.0,因此,可以根据PVx=60.0%和MV1=25.8%而像下式那样倒过来计算初始状态的增益K1。另外,在该初始状态下,阀开度100%时的流量(流量上限值PVh)如上述那样为PVh=100%。Here, the predetermined target flow rate PVx is assumed to be PVx=60.0%. That is, the most standard numerical value given as the flow rate setting value SP of the mass flow controller is SPx=60.0%. Assuming that the initial state valve opening of the mass flow controller for setting the flow rate of the fluid to PVx=60.0% is MV1, MV1=25.8% from the curve cur1. Since the coefficient A=30.0 of the nonlinear characteristic can be known in advance, the gain K1 in the initial state can be calculated inversely as the following formula from PVx=60.0% and MV1=25.8%. In addition, in this initial state, the flow rate (flow rate upper limit value PVh) when the valve opening is 100% is PVh=100% as described above.
K1=PVx/{1.0-exp(-MV1/A)}K1=PVx/{1.0-exp(-MV1/A)}
=60.0/{1.0-exp(-25.8/30.0)}=104.0···(3)=60.0/{1.0-exp(-25.8/30.0)}=104.0···(3)
接下来,获取在经过了发生过滤器的堵塞程度的质量流量控制器的运行时间的时间点的用于维持目标流量PVx的阀开度MV。此时,目标流量PVx是与初始状态的目标流量PVx不同的值即可。此处,目标流量PVx设为40.0%。例如在从运行开始之后经过了72小时的时间点,检测出MV2=16.2%作为用于维持目标流量PVx=40.0%的阀开度MV。该值意味着由于过滤器的堵塞现象而流入至质量流量控制器的点的压力降低,用于维持目标流量PVx=40.0%的阀开度MV必须变为MV2=16.2%。Next, the valve opening MV for maintaining the target flow rate PVx is acquired at the point in time when the operating time of the mass flow controller at which the clogging degree of the filter has occurred has elapsed. In this case, the target flow rate PVx may be a value different from the target flow rate PVx in the initial state. Here, the target flow rate PVx is set to 40.0%. For example, when 72 hours have elapsed from the start of the operation, MV2 = 16.2% is detected as the valve opening MV for maintaining the target flow rate PVx = 40.0%. This value means that the pressure at the point of flow into the mass flow controller decreases due to clogging of the filter, and the valve opening MV for maintaining the target flow rate PVx=40.0% must be changed to MV2=16.2%.
在运行开始之后经过了72小时的时间点的增益K2可以基于PVx=40.0%和MV2=16.2%,如下式那样倒过来计算。The gain K2 at the point in time when 72 hours have passed after the start of the operation can be reversely calculated as in the following formula based on PVx=40.0% and MV2=16.2%.
K2=PVx/{1.0-exp(-MV2/A)}K2=PVx/{1.0-exp(-MV2/A)}
=40.0/{1.0-exp(-16.2/30.0)}=96.0···(4)=40.0/{1.0-exp(-16.2/30.0)}=96.0···(4)
因此,推断增益K在72小时内从初始状态的K1=104.0减少到了K2=96.0,在数值上仅减少了8.0。在该情况下,质量流量控制器的特性变为图1的曲线cur2的样子。并且,在该cur2的状态下,阀开度100%时的流量(流量上限值PVh)能够如下式那样算出。Therefore, the inferred gain K decreased from K1 = 104.0 in the initial state to K2 = 96.0 within 72 hours, a numerical decrease of only 8.0. In this case, the characteristic of the mass flow controller becomes like the curve cur2 of FIG. 1 . And, in the state of this cur2, the flow rate (flow rate upper limit value PVh) when the valve opening degree is 100% can be calculated as the following equation.
PVh=96.0{1.0-exp(-100.0/30.0)}=96.6···(5)PVh=96.0{1.0-exp(-100.0/30.0)}=96.6···(5)
如此,PVh=96.6%为cur2的状态下的可控制的流量的上限值,可以判断为并不是严重的状态。即,成为还不需要质量流量控制器的维护这样的判断指标。In this way, PVh=96.6% is the upper limit value of the controllable flow rate in the state of cur2, and it can be judged that the state is not serious. That is, it becomes a judgment index that the maintenance of the mass flow controller is not required yet.
由于假定增益K与质量流量控制器的运行时间大致成比例地以一定的速度减少,因此能够推断,当从cur2的状态开始再经过大约72小时的时候,恐怕增益K会再减少大约8.0,质量流量控制器的特性会变为图1的曲线cur3(K3=88.0)那样。在该cur3的状态下,阀开度100%时的流量(流量上限值PVh)可以如下式那样算出。但是,仅限于增益K以一定的速度减少的情况。Since it is assumed that the gain K decreases at a constant rate approximately in proportion to the operating time of the mass flow controller, it can be deduced that when about 72 hours have elapsed from the state of cur2, the gain K may decrease by about 8.0, and the mass The characteristic of the flow controller becomes like the curve cur3 (K3=88.0) in FIG. 1 . In this state of cur3, the flow rate (flow rate upper limit value PVh) when the valve opening is 100% can be calculated as follows. However, it is limited to the case where the gain K decreases at a constant speed.
PVh=88.0{1.0-exp(-100.0/30.0)}=84.9···(6)PVh=88.0{1.0-exp(-100.0/30.0)}=84.9···(6)
当整理以上内容时,如下所述。在初始状态(cur1)下,根据PVx=60.0%和MV1=25.8%的实绩可以推断PVh=100%。在从运行开始起经过了72小时后的状态(cur2)下,根据PVx=40.0%和MV2=16.2%的实绩可以推断PVh=96.6%。在又经过72小时之后的状态(cur3)下,可以推断PVh=84.9%。When organizing the above, it is as follows. In the initial state (cur1), PVh=100% can be inferred from the actual performance of PVx=60.0% and MV1=25.8%. In the state (cur2) after 72 hours from the start of the operation, PVh=96.6% can be estimated from actual results of PVx=40.0% and MV2=16.2%. In the state (cur3) after another 72 hours, it can be estimated that PVh=84.9%.
接下来,获取又经过了时间的时间点用于维持目标流量PVx的阀开度MV。此时,设定为目标流量PVx=30.0%,检测到MV4=19.8%。在该情况下,基于PVx=30.0%和MV4=19.8%,可以如下式那样倒过来计算增益K4。Next, the valve opening degree MV for maintaining the target flow rate PVx is acquired at a point in time when time has elapsed. At this time, the target flow rate PVx=30.0% is set, and the detected MV4=19.8%. In this case, based on PVx=30.0% and MV4=19.8%, the gain K4 can be calculated inversely as in the following formula.
K4=PVx/{1.0-exp(-MV4/A)}K4=PVx/{1.0-exp(-MV4/A)}
=30.0/{1.0-exp(-19.8/30.0)}=62.0···(7)=30.0/{1.0-exp(-19.8/30.0)}=62.0···(7)
在该情况下,质量流量控制器的特性如图1的曲线cur4那样。并且,在该cur4的状态下,能够如下式那样算出阀开度100%下的流量(流量上限值PVh)。In this case, the characteristic of the mass flow controller is as shown in the curve cur4 of FIG. 1 . And, in the state of this cur4, the flow rate (flow rate upper limit value PVh) at a valve opening degree of 100% can be calculated as shown in the following equation.
PVh=62.0{1.0-exp(100.0/30.0)}=59.8···(8)PVh=62.0{1.0-exp(100.0/30.0)}=59.8···(8)
如此,PVh=59.8%为cur4状态下的可控制的流量的上限值。作为过去的实绩,有目标流量PVx设为PVx=60.0的例子,由于PVh=59.8%低于过去的目标流量PVx,因此判断为严重的状态。即,成为需要质量流量控制器的维护这样的判断指标。Thus, PVh=59.8% is the upper limit of the controllable flow rate in the cur4 state. As past actual results, there is an example in which the target flow rate PVx is set to PVx=60.0, and since PVh=59.8% is lower than the past target flow rate PVx, it is judged as a severe state. That is, it becomes a judgment index that maintenance of the mass flow controller is required.
根据以上内容,求出质量流量控制器及其相关设备的维护的必要性的判断指标的步骤可以整理为以下的(I)、(II)。根据本实施例,即使在由于是以低流量、低开度(阀开度为充分远离上限的开度)进行控制而看起来阀开度有余量的情况下,也能够得到妥当的判断指标。Based on the above, the steps of obtaining the judgment index for the necessity of maintenance of the mass flow controller and its related equipment can be organized into the following (I) and (II). According to this embodiment, even when it seems that there is a margin in the valve opening due to the low flow rate and low opening degree (the valve opening degree is sufficiently far from the upper limit) for control, an appropriate judgment index can be obtained. .
(I)能够获取用于将流体的流量维持为任意的目标流量PVx的阀开度MV。基于该阀开度MV算出增益K。但是,非线性的系数A是预先规定的。(I) The valve opening MV for maintaining the flow rate of the fluid at an arbitrary target flow rate PVx can be obtained. The gain K is calculated based on the valve opening MV. However, the non-linear coefficient A is predetermined.
K=PVx/{1.0-exp(-MV/A)}···(9)K=PVx/{1.0-exp(-MV/A)}···(9)
(II)算出阀开度MV成为上限100%情况下的流量作为可控制的流量上限值PVh,将该流量上限值PVh作为质量流量控制器及其关联设备是否需要维护的判断指标。(II) Calculate the flow when the valve opening MV reaches 100% of the upper limit as the controllable flow upper limit PVh, and use the flow upper limit PVh as an index for judging whether the mass flow controller and its associated equipment need maintenance.
PVh=K{1.0-exp(-100.0/A)}···(10)PVh=K{1.0-exp(-100.0/A)}···(10)
另外,只要是能够近似出图1的非线性的函数,即便不是指数函数也能运用同样的方法。例如,若是下述的分数函数,则仅靠四则运算便能记述阀开度与流量的非线性。In addition, the same method can be applied even if it is not an exponential function as long as it is a function that can approximate the nonlinearity shown in FIG. 1 . For example, if the following fractional function is used, the nonlinearity between valve opening and flow rate can be described only by four arithmetic operations.
PV=K[{-A/(MV+B)}+C]PV=K[{-A/(MV+B)}+C]
=1.0[{-3130.0/(MV+25.0)}+125.2]···(11)=1.0[{-3130.0/(MV+25.0)}+125.2]···(11)
K=PVx/[{-A/(MV+B)}+C]···(12)K=PVx/[{-A/(MV+B)}+C]···(12)
PVh=K/[{-A/(100.0+B)}+C]···(13)PVh=K/[{-A/(100.0+B)}+C]···(13)
与式(1)同样地,式(11)的函数由常数项(C=125.2)、与阀开度MV有关的项、以及与这些项相乘的增益K加以定义。根据式(11)~式(13),能够以与图1同样的图2表示质量流量控制器的特性。图2的曲线cur1的状态下的增益K1为1.0,曲线cur2的状态下的增益K2为0.923,曲线cur3的状态下的增益K3为0.846,曲线cur4的状态下的增益K4为0.596。即,与图1的例子同样地,增益K与运行时间成比例地以一定的速度减少。Like the expression (1), the function of the expression (11) is defined by a constant term (C=125.2), a term related to the valve opening MV, and a gain K multiplied by these terms. From the formulas (11) to (13), the characteristics of the mass flow controller can be shown in FIG. 2 similar to FIG. 1 . In FIG. 2 , the gain K1 in the state of the curve cur1 is 1.0, the gain K2 in the state of the curve cur2 is 0.923, the gain K3 in the state of the curve cur3 is 0.846, and the gain K4 in the state of the curve cur4 is 0.596. That is, similarly to the example in FIG. 1 , the gain K decreases at a constant rate in proportion to the operation time.
接下来,对本实施例的流量控制装置(质量流量控制器)的构成进行说明。如图3所示,本实施例的流量控制装置具备:流量测量部1,其测量在流路中流动的流体的流量;流量控制部2,其操作阀以使由流量测量部1测量出的流量与目标流量PVx一致;阀开度获取部3,其获取在流量控制中流体的流量被维持在预先规定的目标流量PVx时的阀开度MV;流量上限推断部4,其将假定在阀开度MV的获取的时间点阀开度达到上限(例如100%)的情况下的流量上限值PVh推断为维护判断指标;以及推断结果输出部5,其输出与流量上限推断部4的推断结果有关的信息。Next, the configuration of the flow control device (mass flow controller) of this embodiment will be described. As shown in FIG. 3 , the flow control device of this embodiment includes: a flow measurement unit 1 that measures the flow rate of the fluid flowing in the flow path; a flow control unit 2 that operates the valve so that the flow rate measured by the flow measurement unit 1 The flow rate coincides with the target flow rate PVx; the valve opening acquisition unit 3 acquires the valve opening MV when the flow rate of the fluid is maintained at the predetermined target flow rate PVx during the flow control; the flow rate upper limit estimation unit 4 assumes that the valve opening is The flow upper limit value PVh when the valve opening reaches the upper limit (for example, 100%) at the time point of acquisition of the opening MV is estimated as a maintenance judgment index; information about the results.
接下来,参考图4、图5说明本实施例的流量控制装置的动作。图4是说明流量控制动作的流程图,图5为说明维护判断指标推断动作的流程图。Next, the operation of the flow control device of this embodiment will be described with reference to FIGS. 4 and 5 . FIG. 4 is a flow chart illustrating the flow control operation, and FIG. 5 is a flow chart illustrating the maintenance judgment index estimation operation.
流量测量部1持续地测量在流路(图6的流路105)中流动的流体的流量(图4步骤S100)。该流量测量部1相当于图6的流体传感器103,是设置在质量流量控制器中的公知构成。The flow rate measuring unit 1 continuously measures the flow rate of the fluid flowing in the channel (the channel 105 in FIG. 6 ) (step S100 in FIG. 4 ). This flow measurement unit 1 corresponds to the fluid sensor 103 shown in FIG. 6 and is a well-known structure provided in a mass flow controller.
流量控制部2持续地操作阀(图6的阀104)以使流量测量部1测量出的流体的流量与例如由操作人员设定的目标流量PVx一致(图4步骤S101)。该流量控制部2也是设置在质量流量控制器中的公知构成。The flow rate control unit 2 continuously operates the valve (valve 104 in FIG. 6 ) so that the flow rate of the fluid measured by the flow rate measurement unit 1 coincides with, for example, a target flow rate PVx set by an operator (step S101 in FIG. 4 ). This flow control unit 2 is also a known configuration provided in a mass flow controller.
如此,按照预先规定的每一周期(例如50msec.)来反复执行步骤S100、S101的处理直到例如由操作人员指示结束装置的动作为止(图4步骤S102中的是)。In this way, the processes of steps S100 and S101 are repeatedly executed at predetermined intervals (for example, 50 msec.) until, for example, an operator instructs to end the operation of the device (Yes in step S102 in FIG. 4 ).
另一方面,阀开度获取部3获取流体的流量被维持在目标流量PVx时的阀的开度MV(目标维持阀开度)(图5步骤S200)。具体地说,在从一定时间前开始到当前时间点为止的期间内流量测量部1测量出的流量与目标流量PVx的偏差的绝对值持续地处于规定值以内的情况下,阀开度获取部3判定流体的流量被维持在目标流量PVx,并获取当前时间点的阀开度MV。一定时间t的值作为规定值而被设定在阀开度获取部3中。On the other hand, the valve opening acquisition unit 3 acquires the valve opening MV (target maintenance valve opening) when the flow rate of the fluid is maintained at the target flow rate PVx (step S200 in FIG. 5 ). Specifically, when the absolute value of the deviation between the flow rate measured by the flow rate measurement unit 1 and the target flow rate PVx has been continuously within a predetermined value during the period from a certain time ago to the current time point, the valve opening acquisition unit 3. Determine that the flow rate of the fluid is maintained at the target flow rate PVx, and acquire the valve opening MV at the current point in time. The value of the constant time t is set in the valve opening acquisition unit 3 as a predetermined value.
另外,虽然也可以检测阀开度本身,但在安装上并不是检测严格的阀开度,获取从流量控制部2输出至阀的信号(例如阀开度指示信号或阀驱动电流)并基于该信号来判断阀开度即可。In addition, although it is also possible to detect the valve opening itself, it is not strictly necessary to detect the valve opening in terms of installation. The signal output from the flow control unit 2 to the valve (for example, the valve opening indication signal or the valve driving current) is acquired and based on this Signal to judge the valve opening.
接下来,流量上限推断部4基于由阀开度获取部3获取到的阀开度MV(目标维持阀开度),将假定在该获取时间点阀开度达到上限(例如100%)的情况下的流量上限值PVh推断为可控制的流量这样的判断指标。如图3所示,流量上限推断部4由增益算出部40和流量上限算出部41构成,该增益算出部40算出增益K,该流量上限算出部41算出流量上限值PVh。Next, based on the valve opening degree MV (target maintenance valve opening degree) acquired by the valve opening degree acquisition unit 3, the flow rate upper limit estimation unit 4 assumes that the valve opening degree reaches the upper limit (for example, 100%) at the acquisition time point. The lower flow rate upper limit PVh is estimated as a judgment index of a controllable flow rate. As shown in FIG. 3 , the flow rate upper limit estimation unit 4 is composed of a gain calculation unit 40 which calculates a gain K and a flow rate limit calculation unit 41 which calculates a flow rate upper limit value PVh.
流量上限推断部4的增益算出部40利用式(9)来算出想要算出流量上限值PVh的当前时间点的增益K(图5步骤S201)。式(9)的系数A作为规定值而被设定在流量上限推断部4中。为了掌握该系数A,例如事先进行流量控制装置的流量试验而调查好系数A的值即可。The gain calculation unit 40 of the flow rate upper limit estimation unit 4 calculates the gain K at the current point in time at which the flow rate upper limit value PVh is to be calculated by using Equation (9) (step S201 in FIG. 5 ). The coefficient A of the formula (9) is set in the flow rate upper limit estimation unit 4 as a predetermined value. In order to know the coefficient A, for example, a flow rate test of the flow control device may be performed in advance to investigate the value of the coefficient A.
然后,流量上限推断部4的流量上限算出部41基于由增益算出部40算出的增益K,通过式(10)算出流量上限值PVh(图5步骤S202)。以上,结束流量上限推断部4的处理。Then, the flow upper limit calculating unit 41 of the flow upper limit estimating unit 4 calculates the flow upper limit value PVh by the expression (10) based on the gain K calculated by the gain calculating unit 40 (step S202 in FIG. 5 ). As above, the processing of the flow rate upper limit estimation unit 4 ends.
推断结果输出部5输出流量上限推断部4的推断结果(图5步骤S203)。作为推断结果的输出方法,例如有流量上限值PVh的数值显示、基于流量上限值PVh的警报输出、推断结果的信息向外部的发送等。在警报输出的情况下,在流量上限值PVh不足预先规定的阈值(例如不到60%)时,使通知警报的LED点亮即可。The estimation result output unit 5 outputs the estimation result of the flow rate upper limit estimation unit 4 (step S203 in FIG. 5 ). As an output method of the estimation result, there are, for example, numerical display of the flow rate upper limit PVh, alarm output based on the flow rate upper limit PVh, transmission of information of the estimation result to the outside, and the like. In the case of an alarm output, when the flow rate upper limit value PVh is less than a predetermined threshold value (for example, less than 60%), it is only necessary to turn on the LED for notifying the alarm.
阀开度获取部3、流量上限推断部4以及推断结果输出部5按照规定的每一周期ΔT(例如24小时)来反复执行步骤S200~S203的处理,直至例如由操作人员指示结束装置的动作为止(图5步骤S204中的是)。The valve opening acquisition unit 3, the flow upper limit estimation unit 4, and the estimation result output unit 5 repeatedly perform the processing of steps S200 to S203 in accordance with each predetermined period ΔT (for example, 24 hours), until, for example, an operator instructs to end the operation of the device. So far (Yes in step S204 in FIG. 5).
根据以上内容,在本实施例中,能够在装置的运行中对于流量控制装置及其相关设备(设置于流路上的过滤器等)推断是否需要维护的判断指标(流量上限值PVh)。操作人员能够基于流量控制装置的推断结果来判断是否达到了需要维护的严重情况,所以易于执行半导体制造装置等的运行管理。此外,在本实施例中,由于在半导体制造装置的运行停止中不需要进行使流体流入质量流量控制器的流路的作业,所以能够大幅减少是否需要维护的判断所需要的工夫。Based on the above, in this embodiment, it is possible to infer the judgment indicator (flow upper limit value PVh) whether maintenance is required for the flow control device and its related equipment (filters installed on the flow path, etc.) during the operation of the device. An operator can judge whether or not a serious situation requiring maintenance has been reached based on the estimation result of the flow rate control device, so it is easy to perform operation management of a semiconductor manufacturing device or the like. In addition, in this embodiment, since the work of flowing fluid into the flow path of the mass flow controller is not required during the stoppage of the semiconductor manufacturing apparatus, it is possible to greatly reduce the labor required for determining whether maintenance is required.
另外,在阀开度获取部3判断为流体的流量没有被维持在目标流量PVx的情况下,则无法获取阀开度MV,因此在这种情况下,无法算出流量上限值PVh。In addition, when the valve opening acquiring unit 3 determines that the flow rate of the fluid is not maintained at the target flow rate PVx, the valve opening MV cannot be acquired, and thus the flow rate upper limit value PVh cannot be calculated in this case.
此外,即使在目标流量PVx在中途变化的情况下也能够适用本实施例,但在阀开度获取部3判定流体的流量是否被维持在目标流量PVx的一定时间t(t<ΔT)的期间,目标流量PVx需要被维持在相同的值。当目标流量PVx在一定时间t的期间内改变时,无法进行阀开度MV的获取。In addition, the present embodiment can be applied even when the target flow rate PVx changes halfway, but the valve opening acquisition unit 3 determines whether the flow rate of the fluid is maintained at the target flow rate PVx for a certain period of time t (t<ΔT) , the target flow PVx needs to be maintained at the same value. When the target flow rate PVx changes within a certain period of time t, acquisition of the valve opening degree MV cannot be performed.
此外,流量上限推断部4使用式(12)、式(13)代替式(9)、式(10)来计算增益K和流量上限值PVh。式(12)、式(13)的系数A、B、C作为规定的值而被设定在流量上限推断部4中。为了掌握该系数A、B、C,例如事先进行流量控制装置的流量试验即可。Furthermore, the flow rate upper limit estimation unit 4 calculates the gain K and the flow rate upper limit PVh using Expressions (12) and (13) instead of Expressions (9) and (10). Coefficients A, B, and C of Expression (12) and Expression (13) are set in the flow rate upper limit estimation unit 4 as predetermined values. In order to grasp the coefficients A, B, and C, for example, a flow test of the flow control device may be performed in advance.
此外,在本实施例中,是将图3所示的构成全部设置在流量控制装置(质量流量控制器)内,但并不限于此。也可以将阀开度获取部3、流量上限推断部4以及推断结果输出部5作为维护判断指标推断装置而设置在上位设备(例如可编程逻辑控制器PLC)中,并与包含流量测量部1和流量控制部2的普通的微流量控制器结合使用。In addition, in this embodiment, all the configurations shown in FIG. 3 are provided in the flow control device (mass flow controller), but the present invention is not limited thereto. It is also possible to set the valve opening acquisition unit 3, the flow upper limit estimation unit 4, and the estimation result output unit 5 as a maintenance judgment index estimation device in a host device (such as a programmable logic controller PLC), and together with the flow measurement unit 1 It is used in conjunction with the ordinary micro-flow controller of the flow control unit 2.
在本实施例中所说明的流量控制装置可以通过具备CPU(Central ProcessingUnit中央处理器)、存储装置及接口的计算机和控制这些硬件资源的程序来实现。同样地,由阀开度获取部3、流量上限推断部4以及推断结果输出部5构成的维护判断指标推断装置可以通过计算机和程序来实现。各装置的CPU根据各自的存储装置中存储的程序来执行本实施例中说明过的处理。由此,能够实现本实施例的维护判断指标推断方法。The flow control device described in this embodiment can be realized by a computer including a CPU (Central Processing Unit), a storage device, and an interface, and a program for controlling these hardware resources. Likewise, the maintenance judgment index estimation device composed of the valve opening degree acquisition unit 3 , the flow rate upper limit estimation unit 4 , and the estimation result output unit 5 can be realized by a computer and a program. The CPU of each device executes the processing described in the present embodiment according to the programs stored in the respective storage devices. Thus, the maintenance judgment index estimation method of this embodiment can be realized.
产业上的可利用性Industrial availability
本发明可以适用于管理流量控制装置及其相关设备的技术中。The present invention can be applied to the technology of managing the flow control device and its related equipment.
符号说明Symbol Description
1…流量测量部、2…流量控制部、3…阀开度获取部、4…流量上限推断部、5…推断结果输出部、40…增益算出部、41…流量上限算出部。1...Flow measurement unit, 2...Flow control unit, 3...Valve opening acquisition unit, 4...Flow limit estimation unit, 5...Estimation result output unit, 40...Gain calculation unit, 41...Flow limit calculation unit.
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